modelExercise9TwoStageSteamTurbine

Exercise 8.9: Two-Stage Steam Turbine with Extraction for District Heating [TUM2019]

Extends from Modelica.Icons.Example (Icon for runnable examples).

Information

Example of a steam Rankine combined heat and power (CHP) cycle with a two-stage turbine and an extraction branch for district heating.

English problem description

A steamBoiler supplies steam at p1 = 58.0 bar and T1 = 723 K. In the adiabatic highPressureTurbine, which delivers a power output of 800 kW, the steam expands to p2 = 3.00 bar with an isentropic efficiency of 0.710.

Part of the steam is directed to a heatingNetwork, while the remainder expands in the adiabatic lowPressureTurbine to p3 = 50.0 mbar. The lowPressureTurbine delivers 200 kW at an isentropic efficiency of 0.800. The mechanical efficiencies of the turbine shafts are 0.920.

After the lowPressureTurbine, the water is completely condensed in the condenser. In the heatingNetwork, the steam condenses and the condensate is subcooled to T6 = 323 K. The two mass flows are then pumped by the reversible adiabatic feedwater pumps pump1 and pump2 to the boiler pressure p7 = p8 = p1 and returned to the cycle via the mixer.

The steamBoiler, condenser, heatingNetwork, and mixer operate isobarically. Kinetic and potential energies can be neglected, and liquid water may be treated as incompressible.

Components

TypeNameDefaultDescription
ThermofluidStream.DropOfCommonsdropOfCommons
ThermofluidStream.Idealized.Processes.Adiabaticpump2
ThermofluidStream.Idealized.Processes.AdiabaticlowPressureTurbine
ThermofluidStream.Idealized.Processes.IsobaricsteamBoiler
ThermofluidStream.Idealized.Processes.Isobariccondensor
Modelica.Blocks.Sources.RealExpressionh_bubble
ThermofluidStream.Idealized.Processes.Adiabaticpump1
ThermofluidStream.Idealized.Topology.JunctionT2mixer
ThermofluidStream.Idealized.Processes.AdiabatichighPressureTurbine
ThermofluidStream.Topology.SplitterT2splitter
ThermofluidStream.Idealized.Boundaries.LoopBreakerloopBreaker
ThermofluidStream.Idealized.Processes.IsobaricheatingNetwork
ThermofluidStream.Utilities.showRealValueheatFlowRateHeatingNetwork
ThermofluidStream.Utilities.showRealValueefficiency1
ThermofluidStream.Idealized.EnergyFlow.Sources.FixedEnergyFlowpowerHighPressureTurbine
ThermofluidStream.Idealized.EnergyFlow.Components.FixedTransferEfficiencylossesHPTShaft
ThermofluidStream.Idealized.EnergyFlow.Sources.FixedEnergyFlowpowerLowPressureTurbine
ThermofluidStream.Idealized.EnergyFlow.Components.FixedTransferEfficiencylossesLPTShaft
ThermofluidStream.Utilities.showRealValueefficiency

Contents

NameDescription
Medium

Revisions

  • 2026, by Raphael Gebhart (raphael.gebhart@dlr.de):
    Initial version.